Xueliang Li
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Research Subjects
Research Interests
Xueliang Li has a total of 55 co-authors. Here are the top co-authors by number of shared publications:
Paul Stevenson
Department of Chemical and Materials Engineering, Faculty of Engineering, University of Auckland, New Zealand
8 shared publicationsGeoffrey M. Evans
Centre for Advanced Particle Processing, University of Newcastle, Callaghan, NSW 2308, Australia
5 shared publicationsGuocheng Du
Key Laboratory of Carbohydrate Chemistry and Biotechnology, Ministry of Education, Jiangnan University, Wuxi, China
2 shared publicationsRyan Shaw
Centre for Advanced Particle Processing, University of Newcastle, Callaghan, NSW 2308, Australia
2 shared publications- Zhaoliang Wu
School of Chemical Engineering and Technology, Hebei University of Technology, Tianjin, China
2 shared publications - Andrew J. Sederman
Department of Chemical Engineering and Biotechnology, University of Cambridge, West Cambridge Site, Philippa Fawcett Drive, Cambridge CB3 0AS, United Kingdom
1 shared publication
Latest Publications
- Open Access
- 4 March 2026
- Published by MDPI AG in Fermentation
- Vol. 12 (3) , 134
Metabolic Flux Analysis of Escherichia coli Based on Kinetic Model and Genome-Scale Metabolic Network Model
The application of Genome-Scale Metabolic Network Models (GSMM) in fermentation optimization is hampered by challenges in differentiating viable from dead cells and parameter distortion induced by conventional detection methods. Using E. coli BL21(DE3) as the model organism, this study developed a flux analysis strategy that couples cell kinetics with GSMM. Key parameters were estimated using the gradient descent algorithm, thereby enabling precise prediction of viable cell concentration and glucose consumption dynamics. Integrating this with the Quadratic Programming-based parsimonious Flux Balance Analysis (QP-pFBA) algorithm, intracellular metabolic reaction fluxes were quantified. Results demonstrated that the model can effectively differentiate viable from dead cells; Batch D, adopting the gradient-increasing feeding strategy, achieved the maximum specific growth rate (μmax) of 0.6457, the highest among the four batches. Moreover, key metabolic reaction fluxes were highly correlated with the feeding strategy. This framework forgoes specialized, high-cost equipment and offers robust cross-strain/process adaptability, thereby greatly advancing GSMM utility. It provides a powerful tool for precise fermentation control and accelerates the shift toward data-driven biomanufacturing.
- 4 March 2026
- Published by MDPI AG in Fermentation
- Vol. 12 (3) , 134
Open AccessMetabolic Flux Analysis of Escherichia coli Based on Kinetic Model and Genome-Scale Metabolic Network Model
The application of Genome-Scale Metabolic Network Models (GSMM) in fermentation optimization is hampered by challenges in differentiating viable from dead cells and parameter distortion induced by conventional detection methods. Using E. coli BL21(DE3) as the model organism, this study developed a flux analysis strategy that couples cell kinetics with GSMM. Key parameters were estimated using the gradient descent algorithm, thereby enabling precise prediction of viable cell concentration and glucose consumption dynamics. Integrating this with the Quadratic Programming-based parsimonious Flux Balance Analysis (QP-pFBA) algorithm, intracellular metabolic reaction fluxes were quantified. Results demonstrated that the model can effectively differentiate viable from dead cells; Batch D, adopting the gradient-increasing feeding strategy, achieved the maximum specific growth rate (μmax) of 0.6457, the highest among the four batches. Moreover, key metabolic reaction fluxes were highly correlated with the feeding strategy. This framework forgoes specialized, high-cost equipment and offers robust cross-strain/process adaptability, thereby greatly advancing GSMM utility. It provides a powerful tool for precise fermentation control and accelerates the shift toward data-driven biomanufacturing.
- Open Access
BioDT: An Integrated Digital-Twin-Based Framework for Intelligent Biomanufacturing
The field of industrial biotechnology has shown an increasing interest in adopting digital twins for improving process productivity and management efficiency. Despite its potential benefits, digital-twin-based biomanufacturing has not been fully implemented. As a preliminary undertaking, we developed an open-source digital twin framework for cell culture. The core models of the digital twin were coded in C++ and compiled as a reusable Python library. A web-based, cloud-native HMI application that links the physical and virtual systems was developed. A microbioreactor digital twin system was implemented using the framework as a proof of concept. The system features a 3D-printed rocking platform that is customized to fit T25 flasks, enabling automated rocking rate and angle control and in-place optical cell density measurement. The digital twin was validated using Chinese Hamster Ovary (CHO) cells and was found to be able to predict the changes in cell density, glucose consumption, lactic acid production, and oxygen uptake rate (OUR). Finally, we performed a case study to demonstrate the system’s practical applicability in Advanced Process Control (APC) by constructing real-time glucose and lactic acid soft sensors, which are in turn used to alert the operator for manual media change or for automated feeding.
Open AccessBioDT: An Integrated Digital-Twin-Based Framework for Intelligent Biomanufacturing
The field of industrial biotechnology has shown an increasing interest in adopting digital twins for improving process productivity and management efficiency. Despite its potential benefits, digital-twin-based biomanufacturing has not been fully implemented. As a preliminary undertaking, we developed an open-source digital twin framework for cell culture. The core models of the digital twin were coded in C++ and compiled as a reusable Python library. A web-based, cloud-native HMI application that links the physical and virtual systems was developed. A microbioreactor digital twin system was implemented using the framework as a proof of concept. The system features a 3D-printed rocking platform that is customized to fit T25 flasks, enabling automated rocking rate and angle control and in-place optical cell density measurement. The digital twin was validated using Chinese Hamster Ovary (CHO) cells and was found to be able to predict the changes in cell density, glucose consumption, lactic acid production, and oxygen uptake rate (OUR). Finally, we performed a case study to demonstrate the system’s practical applicability in Advanced Process Control (APC) by constructing real-time glucose and lactic acid soft sensors, which are in turn used to alert the operator for manual media change or for automated feeding.
- Top Cited Papers
- 1 March 2021
- Published by Springer Nature in Systems Microbiology and Biomanufacturing
- Vol. 1 (3) , 257-274
Digital Twin in biomanufacturing: challenges and opportunities towards its implementation
- 1 March 2021
- Published by Springer Nature in Systems Microbiology and Biomanufacturing
- Vol. 1 (3) , 257-274
Top Cited PapersDigital Twin in biomanufacturing: challenges and opportunities towards its implementation
- 7 September 2020
- Published by Springer Nature in Nature Chemical Biology
- Vol. 16 (11) , 1261-1268
Pyruvate-responsive genetic circuits for dynamic control of central metabolism
Dynamic regulation is a promising strategy for fine-tuning metabolic fluxes in microbial cell factories. However, few of these synthetic regulatory systems have been developed for central carbon metabolites. Here we created a set of programmable and bifunctional pyruvate-responsive genetic circuits for dynamic dual control (activation and inhibition) of central metabolism in Bacillus subtilis. We used these genetic circuits to design a feedback loop control system that relies on the intracellular concentration of pyruvate to fine-tune the target metabolic modules, leading to the glucaric acid titer increasing from 207 to 527 mg l−1. The designed logic gate-based circuits were enabled by the characterization of a new antisense transcription mechanism in B. subtilis. In addition, a further increase to 802 mg l−1 was achieved by blocking the formation of by-products. Here, the constructed pyruvate-responsive genetic circuits are presented as effective tools for the dynamic control of central metabolism of microbial cell factories.
- 7 September 2020
- Published by Springer Nature in Nature Chemical Biology
- Vol. 16 (11) , 1261-1268
Pyruvate-responsive genetic circuits for dynamic control of central metabolism
Dynamic regulation is a promising strategy for fine-tuning metabolic fluxes in microbial cell factories. However, few of these synthetic regulatory systems have been developed for central carbon metabolites. Here we created a set of programmable and bifunctional pyruvate-responsive genetic circuits for dynamic dual control (activation and inhibition) of central metabolism in Bacillus subtilis. We used these genetic circuits to design a feedback loop control system that relies on the intracellular concentration of pyruvate to fine-tune the target metabolic modules, leading to the glucaric acid titer increasing from 207 to 527 mg l−1. The designed logic gate-based circuits were enabled by the characterization of a new antisense transcription mechanism in B. subtilis. In addition, a further increase to 802 mg l−1 was achieved by blocking the formation of by-products. Here, the constructed pyruvate-responsive genetic circuits are presented as effective tools for the dynamic control of central metabolism of microbial cell factories.
- 1 January 2020
- Published by Elsevier in Chemical Engineering Science
- Vol. 211
A conceptual air-lift reactor design for large scale animal cell cultivation in the context of in vitro meat production
- 1 January 2020
- Published by Elsevier in Chemical Engineering Science
- Vol. 211
A conceptual air-lift reactor design for large scale animal cell cultivation in the context of in vitro meat production
- 1 January 2018
- Published by Elsevier in Biochemical Engineering Journal
- Vol. 129, 64-73
Experimental testing of a spatiotemporal metabolic model for carbon monoxide fermentation with Clostridium autoethanogenum
- 1 January 2018
- Published by Elsevier in Biochemical Engineering Journal
- Vol. 129, 64-73
Experimental testing of a spatiotemporal metabolic model for carbon monoxide fermentation with Clostridium autoethanogenum
- 1 June 2012
- Published by Elsevier in International Journal of Multiphase Flow
- Vol. 42, 24-28
Remarks on approaches that relate foam drainage rate to bubble terminal velocity
- 1 June 2012
- Published by Elsevier in International Journal of Multiphase Flow
- Vol. 42, 24-28
Remarks on approaches that relate foam drainage rate to bubble terminal velocity
- 17 February 2012
- Published by American Chemical Society (ACS) in Langmuir
- Vol. 28 (9) , 4060-4068
Effect of Environmental Humidity on Static Foam Stability
The quality of foaming products (such as beer and shampoo) and the performance of industrial processes that harness foam (such as the froth flotation of minerals or the foam fractionation of proteins) depend upon foam stability. In this study, experiments are performed to study the effect of environmental humidity on the collapse of static foams. The dependency of the rate at which a foam collapses upon humidity is demonstrated, and we propose a hypothesis for bubble bursting due to Marangoni instability induced by nonuniform evaporation to help explain the dependency. This hypothesis is supported by direct experimental observations of the bursting process of isolated bubbles by high speed video recording and the thinning of isolated foam films under different values of humidity and temperature by microinterferometric methods.
- 17 February 2012
- Published by American Chemical Society (ACS) in Langmuir
- Vol. 28 (9) , 4060-4068
Effect of Environmental Humidity on Static Foam Stability
The quality of foaming products (such as beer and shampoo) and the performance of industrial processes that harness foam (such as the froth flotation of minerals or the foam fractionation of proteins) depend upon foam stability. In this study, experiments are performed to study the effect of environmental humidity on the collapse of static foams. The dependency of the rate at which a foam collapses upon humidity is demonstrated, and we propose a hypothesis for bubble bursting due to Marangoni instability induced by nonuniform evaporation to help explain the dependency. This hypothesis is supported by direct experimental observations of the bursting process of isolated bubbles by high speed video recording and the thinning of isolated foam films under different values of humidity and temperature by microinterferometric methods.